CN1521879A - Interconnect device, fuel cell and fuel cell stack - Google Patents

Interconnect device, fuel cell and fuel cell stack Download PDF

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Publication number
CN1521879A
CN1521879A CNA2004100050666A CN200410005066A CN1521879A CN 1521879 A CN1521879 A CN 1521879A CN A2004100050666 A CNA2004100050666 A CN A2004100050666A CN 200410005066 A CN200410005066 A CN 200410005066A CN 1521879 A CN1521879 A CN 1521879A
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channels
channel
fuel cell
interconnect
layer
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CN1316657C (en
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C���¶�ɭ
C·奥尔森
3
H·尤斯特鲁德
�������ɭ
J·U·尼尔森
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Topsoe AS
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Haldor Topsoe AS
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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0247—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
    • H01M8/0254—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form corrugated or undulated
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/14—Fuel cells with fused electrolytes
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
    • H01M8/244—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes with matrix-supported molten electrolyte
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2457—Grouping of fuel cells, e.g. stacking of fuel cells with both reactants being gaseous or vaporised
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465—Details of groupings of fuel cells
    • H01M8/2483—Details of groupings of fuel cells characterised by internal manifolds
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465—Details of groupings of fuel cells
    • H01M8/2484—Details of groupings of fuel cells characterised by external manifolds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00781—Aspects relating to microreactors
    • B01J2219/00783—Laminate assemblies, i.e. the reactor comprising a stack of plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00781—Aspects relating to microreactors
    • B01J2219/00851—Additional features
    • B01J2219/00853—Employing electrode arrangements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00781—Aspects relating to microreactors
    • B01J2219/00851—Additional features
    • B01J2219/00869—Microreactors placed in parallel, on the same or on different supports
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00781—Aspects relating to microreactors
    • B01J2219/00873—Heat exchange
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00781—Aspects relating to microreactors
    • B01J2219/00891—Feeding or evacuation
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/06—Integration with other chemical processes
    • C01B2203/066—Integration with other chemical processes with fuel cells
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • H01M2008/1293—Fuel cells with solid oxide electrolytes
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
    • H01M8/0637—Direct internal reforming at the anode of the fuel cell
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells

Abstract

The invention provides an interconnect device for a fuel cell comprising an electrolyte, an anode and a cathode, the interconnect device comprising a channel system having a plurality of channels, each channel being closed in one end and having either an inlet side or an outlet side at the open end of the channel, each channel having an inlet side placed in alternating order with a channel having an outlet side, the inlet side of each channel placed in consecutive order on one side of the interconnect, and the outlet sides of each channel placed in consecutive order on the opposide side of the interconnect relative to the inlet side, and a second layer of channels is located on the surface of the channel system. The invention also provides a fuel cell and a fuel cell stack in which the interconnect device is used.

Description

Interconnect device, fuel cell and fuel cell stack
Technical Field
The invention relates to a high-temperature fuel cell, in particular a Solid Oxide Fuel Cell (SOFC) or a Molten Carbonate Fuel Cell (MCFC), in which reforming of hydrocarbons takes place in an anode chamber or in an anode. In particular, the invention relates to an interconnection device in a fuel cell of the SOFC type or MCFC type, in which the mechanical tensions inside the fuel cell are relieved.
Background
Solid oxide fuel cells comprise an oxygen-ion conducting electrolyte, a cathode where oxygen is reduced and an anode where hydrogen is oxidized. The overall reaction in a solid oxide fuel cell is: the hydrogen and oxygen electrochemically react to produce electricity, heat, and water.
The anode also contains high catalytic activity for steam reforming of hydrocarbons to hydrogen, carbon dioxide and carbon monoxide. Steam reforming can be described by the reaction of a fuel, such as natural gas, with steam, and the reaction that occurs can be represented by the following equation:
the fuel gas supplied to the fuel cell contains steam in most cases, whereby a steam reforming process can be performed at the anode surface according to the above equation. Then, the generated hydrogen reacts in the above electrochemical reaction. However, the steam reforming reaction is very endothermic, and therefore requires a large input of heat.
Typical temperature profiles in fuel cell stacks using hydrocarbon feeds show a significant temperature drop near the fuel cell inlet, due to the rapid endothermic reforming reaction that results in significant temperature gradients withinthe cell.
A solid oxide fuel cell is a ceramic composite formed from three different materials. Ceramic solid oxide fuel cells have a low mechanical strength, in particular a low tensile strength. The tensile strength inside the solid oxide fuel cell is closely related to the temperature gradient, and therefore it becomes very important to minimize the temperature gradient, and thus the tensile strength of the solid oxide fuel cell. When the tensile strength in the fuel cell exceeds a given threshold value, the cell will crack and the fuel cell will fail.
By using hydrogen feed, it is possible to some extent to adjust the tensile strength to an acceptable level, but natural gas and other hydrocarbon feeds are expected to dominate in the future. This significantly exacerbates the problem, as endothermic reforming of hydrocarbons will significantly reduce the temperature of the fuel cell at the fuel inlet region, thereby increasing the temperature gradient and tensile strength within the fuel cell to an unacceptable level.
Various methods of reducing the temperature gradient are known. Most of these methods involve changes in the operating parameters of the fuel cell system, such as stronger gas flow to the cathode. Such changes are often associated with increased operating costs of the battery system.
Disclosure of Invention
The object of the present invention is to reduce the thermal gradient and tensile strength of a fuel cell by using an interconnect means for dividing the fuel into a plurality of micro fuel cells. This can be achieved by distributing the fuel gas supply of the fuel cell over the entire surface of the cell. In this way, many small electrochemical cells are formed on one fuel cell. The tensile strength of the cell is greatly reduced due to the short thermal path between the reforming reaction, which requires heat, and the electrochemical reaction, which generates heat.
According to the present invention there is therefore provided an interconnect for a fuel cell comprising an electrolyte, an anode and a cathode, the interconnect comprising a channel system having a plurality of channels, each channel being closed at one end and having an inlet side or an outlet side at the open end of the channel. The channels having an inlet side are arranged alternately with the channels having an outlet side, the inlet side of the channels being arranged in a consecutive order on one side of the interconnect, the outlet side of the channels being arranged in a consecutive order on the opposite side of the interconnect with respect to the inlet side, and the second layer of channels being located on the surface of the channel system.
The invention also provides a fuel cell comprising an electrolyte, an anode, a cathode and an interconnect.
Further, the present invention provides a fuel cell stack comprising at least two fuel cells.
Drawings
FIGS. 1 and 1a show an interconnect device having open gas supply and collection channels;
FIGS. 2 and 2a show an interconnection of open gas supply and collection channels with surface channels at right angles;
FIGS. 3 and 3a show an interconnect device having enclosed gas supply and collection channels and apertures in the interconnect surface;
FIGS. 4 and 4a show an interconnect device having partially enclosed gas supply and collection channels with surface channels at right angles;
FIG. 5 shows a top view of an interconnectdevice; and
fig. 6 shows a cross-sectional view of an assembled fuel cell stack.
Detailed Description
Reducing the temperature gradient within the fuel cell can be accomplished by ensuring that the fuel gas is distributed across the cell surface, thereby allowing the endothermic reforming reaction and the exothermic electrochemical reaction to occur uniformly over the cell surface. The pressure gradient ensures a uniform gas flow over most of the area of the cell.
The interconnect according to the invention is primarily suitable for high temperature applications on the fuel gas side, i.e. the anode side, of the fuel cell. The oxygen side, i.e. the cathode side, of the interconnect may have any geometry suitable for oxygen delivery. For example, may be straight, parallel channels or any other type of channel known in the art.
The exact path of fuel flow may vary and give multiple fuel paths. Different embodiments of the interconnect according to the present invention are described below, each describing a different configuration of the interconnect and thus a different fuel flow path.
The following table gives a list of the different part numbers of the interconnection means shown in the figures:
numbering interconnect device portion
1 feed hole
2 feed channel
3 link surface
4 collecting channel
5 discharge hole
6 channel second layer
7 dispensing hole
8 collecting hole
Fig. 1 shows a simple interconnect geometry in which fuel flows from feed holes 1 and through a porous anode arranged on the surface 3 of the interconnect on the way from feed channels 2 to collection channels 4. This embodiment has a channel system comprising open gas supply and collection channels. By open channel is meant that the upper surface of the channel is uncovered or not closed over its length. By closed channel is meant that the upper surface of the channel is covered in the direction of its length.
A more detailed explanation of the fuel gas passage through the anode side is as follows:
fuel enters the interconnect from one or more fuel feed holes 1. The fuel is distributed through the anode via feed channels 2 in the interconnect. The fuel is exposed to the anode material. If the fuel is a hydrocarbon, the fuel reacts endothermically with steam upon contact with the anode material. The fuel is then consumed in an exothermic electrochemical reaction to generate electricity. The two reactions occur in close proximity to each other and benefit each other because the reforming reaction takes advantage of the heat generated by the electrochemical reaction. This spent fuel waste is collected in the interconnect by the channel 4 and directed to the drain holes 5 at the periphery of the cell.
Figure 1a shows a side view of the passage of fuel gas through the interconnect and anode. The anode is arranged on the interconnect surface 3 and gas transport takes place from the feed channel 2 via the anode to the collecting channel 4.
In the embodiment shown in fig. 1, the feed and collection channels are straight, parallel channels. The channels are not limited to straight, parallel channels, but may have other geometries, such as diagonally placed.
In a second embodiment, the fuel flow is not restricted to passing entirely through the porous anodematerial. It may also partially flow through the gap created between the anode surface and the interconnect surface. This reduces the pressure drop. Such gaps are obtained by making a second layer 6 of channels in the interconnection surface 3, which gaps form an angle with the feed and collection channels 2 and 4: they intersect the channels in the channel system and are located on the surface of the channel system as shown in fig. 1. As shown in fig. 2, in which the interconnect has open feed and collection channels with surface channels 6 formed perpendicular to the feed and collection channels. Other angles may be chosen so that the surface channel second layer 6 does not form a right angle with the feed and collection channels 2 and 4. The surface channel second layer 6, which is closed at both ends, may for example be placed diagonally with respect to the feed and collection channels 2 and 4.
Fig. 2a shows a side view of a channel through which fuel gas flows. Gas transport takes place from the feed channel via the second layer 6 of channels to the collecting channel. During gas transport, the gas contacts the anode placed on the interconnect surface 3 and is steam reformed.
In a third embodiment the feed channel is closed and the closed interconnect surface 3 is perforated in the area of the channel. In this embodiment the closed, perforated surface 3 corresponds to a second layer of channels which are closed at their surface and both ends and perforated in the channel area. The channels of the second layer are arranged parallel to and directly above those of the channel system. This ensures that fuel passing through the perforations is reformed only in the region near the perforations. Figure 3 shows an interconnect with closed gas feed and collection channels, where the fuel flows through the perforations in the interconnect surface 3 over the feed channels and into the porous anode material. The reformed gas leaves the anode and entersthe collecting channel through perforations arranged in the collecting channel 4.
Fig. 3a shows a small fuel distribution opening 7 in the feed channel 2 and a fuel waste collection opening 8 in the collection channel 4.
In the fourth embodiment, the fuel flow partially flows through the second layer 6 of surface channels in the interconnection surface 3, which are at an angle to the feed and collection channels 2 and 4. This reduces the pressure drop. As shown in fig. 4, in which the second layer 6 of surface channels is perpendicular to the feed and collection channels 2 and 4 of the channel system. The feed and collection channels 2 and 4 are partially closed. The second layer 6 of surface channels may also be placed at another angle, e.g. diagonally, to the feed and collection channels 2 and 4. They are closed at both ends.
Fig. 4a shows a side view of a channel through which the fuel gas flows, showing the fuel distribution holes 7 present in the feed channel 2 and the waste collection holes 8 in the collection channel 4.
In various embodiments, it may be practical to use two or more intermediate layers instead of a single layer to form the anode side of the interconnect. This can be carried out, for example, by forming one intermediate layer provided with the channel system and placing a second intermediate layer provided with a second layer of channels on the surface of the first intermediate layer.
Fig. 5 shows a top view of the anode side of the interconnect device. The figure shows the embodiment depicted in fig. 4, wherein the interconnect has partially enclosed gas feed and collection channels. The figure shows the structure of many small electrochemical cells produced on one fuel cell.
The fuel cell is placed on the interconnect upper surface 3 with its anode side facing the interconnect means. The fuel cell should be tightly sealed along the edges of the interconnect to prevent all of the fuel gas from flowing along other passageways than the intended passageway.
The hydrocarbon-containing fuel gas is supplied to the interconnect through a plurality of feed holes 1 connected to closed fuel gas feed channels 2. A number of small fuel supply distribution apertures 7 in the feed channels 2 allow fuel to flow out of the feed channels 2 to expose them to the anode side of the fuel cells at the top of the interconnect. The fuel will flow out of the distribution apertures 7, past the surface of the second layer 6 of channels, to the fuel waste collection apertures 8 which communicate the gas with the enclosed fuel waste collection channels 4. During its transport, the gas contacts the anode and is steam reformed. From the collecting channel 4, the reformed fuel gas exits the interconnect through the fuel waste discharge hole 5. The reformed fuel gas includes hydrogen, which reacts with oxygen in a total electrochemical reaction to generate electrical energy, heat, and water. The waste products exiting the anode side of the interconnect are thus primarily carbon dioxide and water. The fuel gas flow may be controlled by a pressure differential between the fuel gas supply and the fuel gas waste.
The interconnect means in the present invention may if desired have distribution holes 7 and collection holes 8 arranged in the feed and collection channels 2 and 4. This ensures that the supply of fresh fuel gas is distributed over the entire surface of the fuel cell before exposure to the anode. By using the interconnect in the fuel cell in the case where the fuel gas contains hydrocarbons, the endothermic reforming reaction is distributed uniformly over the surface of the fuel cell. The simultaneous electrochemical reactions are distributed evenly over the surface of the fuel cell so that the waste heat generated by this reaction is used for the reforming reaction. The temperature difference between the fuel supply distribution hole 7 and the fuel scrap collecting hole 8, which is generated due to the difference between the waste heat generated by the electrochemical reaction and the heat consumption of the reforming reaction, is minimized due to the short heat transfer distance. This heat transfer will be primarily by way of heat conduction in the interconnect and the fuel cell.
As a result of the minimization of the temperature gradient, it is further achieved that mechanical stresses in the fuel cell due to the temperature gradient are minimized, thereby reducing the chance of mechanical failure of the fuel cell. This gradient will be minimized for any type of fuel gas used, but is generally most advantageous where the hydrocarbon feedstock contacts the anode for reforming.
Figure 6 shows a cross-sectional view of an assembled fuel cell stack showing the position of the interconnect relative to other components of the fuel cell. There are five layers shown in the figure, the top layer showing the interconnect means placed on the cathode 10. An oxygen supply channel 9 provides oxygen for the reaction taking place at the cathode and is located on the cathode side of the interconnect. The geometry of the oxygen supply channel 9 may be selected to facilitate the transfer of a desired amount of oxygen to the cathode. The oxygen supply channels may be formed as, for example, straight, parallel channels. Other geometries known in the art may also be used.
A cathode 10 is placed between the interconnect and the electrolyte layer 11. This is followed by an anode layer 12, the other surface of which is in contact with the interconnect surface 3.
The two contact surfaces of the interconnect means may be provided in different ways, for example by contacting two intermediate layers with each other, one intermediate layer having an anode side provided with a fuel gas supply system according to different embodiments of the invention; the other intermediate layer has a cathode side with an oxygen supply system as used in the conventional art. Together, the two intermediate layers provide such an interconnection means.
The interconnect device of the present invention can be used in fuel cells employing internal or external manifolds.

Claims (12)

1. An interconnect for a fuel cell comprising an electrolyte, an anode and a cathode, the interconnect comprising a channel system with a plurality of channels, each channel being closed at one end and having an inlet side or an outlet side at the open end of the channel, the channels having an inlet side being arranged alternately with the channels having an outlet side, the inlet side of the channels being arranged in a consecutive order on one side of the interconnect and the outlet side of the channels being arranged in a consecutive order on the opposite side of the interconnect with respect to the inlet side, and a second layer of channels being located on the surface of the channel system.
2. Interconnection device according to claim 1, characterized in that the channel system has a plurality of straight, parallel channels.
3. Interconnection means according to any one of claims 1 and 2, characterized in that the channel second layer intersects a channel in the channel system, which channel second layer is closed at both ends and the channel of the channel system remains open over its entire length.
4. Interconnection means according to any one of claims 1 and 2, characterized in that the channel second layer is closed at its surface and both ends and that the channel second layer is arranged parallel to and directly above the channels in the channel system, the closed surface being perforated in the area of the channels.
5. Interconnection means according to claim 4, characterized in that the closed, perforated surface of the channel system comprises a separate intermediate layer placed on the surface of the channel system.
6. Interconnection means according to any one of claims 1 and 2, characterized in that a second layer of channels is present on the surface of the channel system, which second layer of channels intersects the channels in the channel system, which second layer of channels is closed at both ends, the channels of the channel system being partly closed.
7. Interconnection means according to any of claims 3 and 6, characterized in that the channel second layer comprises a separate intermediate layer placed on the surface of the channel system.
8. Interconnection means according to any one of claims 1-7, characterized in that the channels of the channel system are provided with distribution and collection openings.
9. A fuel cell comprising an electrolyte, an anode, a cathode and an interconnect according to any one of claims 1 to 8.
10. The fuel cell according to claim 9, wherein the fuel cell is a high temperature fuel cell.
11. The fuel cell of claim 10, wherein the fuel cell is a solid oxide fuel cell or a molten carbonate fuel cell.
12. A fuel cell stack comprising at least two fuel cells according to claim 9, 10 or 11.
CNB2004100050666A 2003-02-15 2004-02-16 Interconnect device, fuel cell and fuel cell stack Expired - Fee Related CN1316657C (en)

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DKPA200300232 2003-02-15
DKPA200300232 2003-02-15

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CN1521879A true CN1521879A (en) 2004-08-18
CN1316657C CN1316657C (en) 2007-05-16

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US (1) US7297425B1 (en)
EP (1) EP1447869A1 (en)
JP (1) JP2004247305A (en)
CN (1) CN1316657C (en)
AU (1) AU2004200582B2 (en)
CA (1) CA2457180A1 (en)
HK (1) HK1066922A1 (en)
NO (1) NO20040649L (en)

Cited By (4)

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US20070269704A1 (en) 2007-11-22

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